ES284716A1 - Improved procedure for obtaining gas from ammonium synthesis (Machine-translation by Google Translate, not legally binding) - Google Patents

Improved procedure for obtaining gas from ammonium synthesis (Machine-translation by Google Translate, not legally binding)

Info

Publication number
ES284716A1
ES284716A1 ES284716A ES284716A ES284716A1 ES 284716 A1 ES284716 A1 ES 284716A1 ES 284716 A ES284716 A ES 284716A ES 284716 A ES284716 A ES 284716A ES 284716 A1 ES284716 A1 ES 284716A1
Authority
ES
Spain
Prior art keywords
primary
product
reforming
translation
reform
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
ES284716A
Other languages
Spanish (es)
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Harper Marshall Walton
Original Assignee
Harper Marshall Walton
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Harper Marshall Walton filed Critical Harper Marshall Walton
Priority to ES284716A priority Critical patent/ES284716A1/en
Publication of ES284716A1 publication Critical patent/ES284716A1/en
Expired legal-status Critical Current

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Abstract

Improved procedure for the production of ammonia synthesis gas, from hydrocarbons, by the measures of primary catalytic reforming of the hydrocarbons with steam by the use of external combustion gases, catalytically reforming with the air, the product of the primary reform, convert the product of the secondary reform transformed, cool the product of the transfer conversion to condense the content vapor and separate it from the synthesis gas, characterized in that a proportion of steam is maintained in the first phase of primary reform at least 4.5 carbon and a pressure of at least 290 psia is maintained in the secondary reformer phase vaporizing water in an amount of at least about three moles per mole of carbon in the hydrocarbon feedstock added to the primary reformation and at a temperature in the range of 430º F to 500º F by heat exchange with at least one of the products of the Class consisting of said combustion gases and secondary reforming product and admitting vaporized vapor in the primary reforming zone. (Machine-translation by Google Translate, not legally binding)
ES284716A 1963-01-31 1963-01-31 Improved procedure for obtaining gas from ammonium synthesis (Machine-translation by Google Translate, not legally binding) Expired ES284716A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
ES284716A ES284716A1 (en) 1963-01-31 1963-01-31 Improved procedure for obtaining gas from ammonium synthesis (Machine-translation by Google Translate, not legally binding)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
ES284716A ES284716A1 (en) 1963-01-31 1963-01-31 Improved procedure for obtaining gas from ammonium synthesis (Machine-translation by Google Translate, not legally binding)

Publications (1)

Publication Number Publication Date
ES284716A1 true ES284716A1 (en) 1963-06-01

Family

ID=66651230

Family Applications (1)

Application Number Title Priority Date Filing Date
ES284716A Expired ES284716A1 (en) 1963-01-31 1963-01-31 Improved procedure for obtaining gas from ammonium synthesis (Machine-translation by Google Translate, not legally binding)

Country Status (1)

Country Link
ES (1) ES284716A1 (en)

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